1989
DOI: 10.1209/0295-5075/10/1/005
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Fingering Instabilities of Driven Spreading Films

Abstract: We show that a thin film with small dynamic contact angle and driven by an external body force is unstable to the formation of fingers in the direction perpendicular to the main flow. The instability is largest in the capillary region near the contact line, where the force due to surface tension is comparable to the viscous and gravitational forces. The fastest growing wavelength is calculated in the limit of small-amplitude disturbances. These instabilities may be related to finger patterns observed in gravit… Show more

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Cited by 317 publications
(326 citation statements)
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“…[20][21][22] The reader is referred to these references for an in depth discussion. This mechanism is quite different, however, from the fingering behavior observed at the leading edge of other free surface spreading problems, like the flow down an inclined plane 30,31 or the thermocapillary driven spreading of a thin liquid film. 32,33 In these other spreading processes, the instability occurs right at the leading edge and causes the spreading front to separate into long narrow rivulets which never undergo spreading, shielding, or tip-splitting.…”
Section: A Linearized Transient Responsementioning
confidence: 61%
“…[20][21][22] The reader is referred to these references for an in depth discussion. This mechanism is quite different, however, from the fingering behavior observed at the leading edge of other free surface spreading problems, like the flow down an inclined plane 30,31 or the thermocapillary driven spreading of a thin liquid film. 32,33 In these other spreading processes, the instability occurs right at the leading edge and causes the spreading front to separate into long narrow rivulets which never undergo spreading, shielding, or tip-splitting.…”
Section: A Linearized Transient Responsementioning
confidence: 61%
“…The limitR → ∞ for both flow down the outside and inside of a cylinder corresponds to the very well studied equation for flow down a vertical plane (α = π/2) [1,4,5,7,18]. By observing that β = 0 removes substrate curvature completely from the model (1), we use this value of β as a 'control' against which we compare our results for β = 1 (outside a cylinder) and −1 (inside a cylinder).…”
Section: C379mentioning
confidence: 99%
“…Our model is also analogous to that describing the flow of thin fluid films sliding down an inclined plane. Adopting the lubrication approximation [46,50,77,49,18], the evolution equation of the film height h can be written as…”
Section: Related Models In Fluid Mechanicsmentioning
confidence: 99%
“…For completely wetting fluids, Troian et al [77] proposed to model the contact line dynamics by assuming a precursor film of (small) thickness b downstream of the front. In our context, this precursor film corresponds to the initial water saturation.…”
Section: Related Models In Fluid Mechanicsmentioning
confidence: 99%
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